TW200420535A - Heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acid - Google Patents
Heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acidInfo
- Publication number
- TW200420535A TW200420535A TW93105178A TW93105178A TW200420535A TW 200420535 A TW200420535 A TW 200420535A TW 93105178 A TW93105178 A TW 93105178A TW 93105178 A TW93105178 A TW 93105178A TW 200420535 A TW200420535 A TW 200420535A
- Authority
- TW
- Taiwan
- Prior art keywords
- acrolein
- acrylic acid
- gas phase
- phase oxidation
- partial gas
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
Abstract
In a process for partially oxidizing acrolein to acrylic acid in the gas phase under heterogeneous catalysis, the starting reaction gas mixture is oxidized at an acrolein loading of ≤145 and ≥70 I (STP) of acrolein/l of fixed catalyst bed.h over a fixed catalyst bed which is accommodated in two successive reaction zones A, B, the highest temperature of the reaction gas mixture within reaction zone A being above the highest temperature of the reaction gas mixture within reaction zone B.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2003113211 DE10313211A1 (en) | 2003-03-25 | 2003-03-25 | Partial oxidation of acrolein to acrylic acid by conducting starting reaction gas mixture comprising acrolein, molecular oxygen, and inert gas(es) in one reaction stage over fixed catalyst bed comprising multimetal oxide(s) |
US47579403P | 2003-06-05 | 2003-06-05 |
Publications (2)
Publication Number | Publication Date |
---|---|
TW200420535A true TW200420535A (en) | 2004-10-16 |
TWI324994B TWI324994B (en) | 2010-05-21 |
Family
ID=32946129
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW93105178A TWI324994B (en) | 2003-03-25 | 2004-02-27 | Heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acid |
Country Status (6)
Country | Link |
---|---|
CN (1) | CN100378058C (en) |
DE (1) | DE10313211A1 (en) |
ES (1) | ES2545257T3 (en) |
MY (1) | MY136503A (en) |
TW (1) | TWI324994B (en) |
ZA (1) | ZA200508593B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007019597A1 (en) | 2007-04-24 | 2008-05-15 | Basf Ag | Partial gas phase oxidation of acrolein to acrylic acid or methacrolein to methacrylic acid, useful e.g. as monomer to prepare polymers, comprises using a tube bundle reactor in reaction tube of a vertically arranged reaction tubes |
DE102007025869A1 (en) | 2007-06-01 | 2008-07-03 | Basf Se | To service tube bundle of gas-phase hydrocarbon oxidation reactor immediately prior to re-charging with fresh bed of catalyst solids, they are brushed internally |
DE102007028333A1 (en) | 2007-06-15 | 2008-12-18 | Basf Se | Method for introducing a subset taken from at least one production batch of annular shell catalysts K into a reaction tube of a tube bundle reactor |
CN102992996B (en) * | 2011-09-08 | 2015-05-13 | 中国石油天然气股份有限公司 | Preparation method of acrylic acid |
CN107282059B (en) * | 2016-04-13 | 2020-08-07 | 中国石油化工股份有限公司 | Catalyst for producing acrylic acid |
CN109305905B (en) * | 2017-07-28 | 2021-06-18 | 中国石油化工股份有限公司 | Method for synthesizing acrylic acid |
CN110586121A (en) * | 2018-06-12 | 2019-12-20 | 中国石油化工股份有限公司 | Supported acrylic acid catalyst |
CN110586074A (en) * | 2018-06-12 | 2019-12-20 | 中国石油化工股份有限公司 | Catalyst for acrylic acid production |
CN111068653A (en) * | 2018-10-18 | 2020-04-28 | 中国石油化工股份有限公司 | Catalyst for synthesizing acrylic acid from acrolein and application thereof |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
MY121878A (en) * | 1999-03-10 | 2006-02-28 | Basf Ag | Method for the catalytic gas-phase oxidation of propene into acrylic acid |
JP4426069B2 (en) * | 2000-06-12 | 2010-03-03 | 株式会社日本触媒 | Acrylic acid production method |
-
2003
- 2003-03-25 DE DE2003113211 patent/DE10313211A1/en not_active Withdrawn
-
2004
- 2004-02-27 MY MYPI20040689 patent/MY136503A/en unknown
- 2004-02-27 TW TW93105178A patent/TWI324994B/en active
- 2004-03-20 CN CNB2004800080960A patent/CN100378058C/en not_active Expired - Lifetime
- 2004-03-20 ES ES04722172.6T patent/ES2545257T3/en not_active Expired - Lifetime
-
2005
- 2005-10-24 ZA ZA200508593A patent/ZA200508593B/en unknown
Also Published As
Publication number | Publication date |
---|---|
TWI324994B (en) | 2010-05-21 |
CN100378058C (en) | 2008-04-02 |
ES2545257T3 (en) | 2015-09-09 |
DE10313211A1 (en) | 2004-10-07 |
MY136503A (en) | 2008-10-31 |
ZA200508593B (en) | 2007-02-28 |
CN1764631A (en) | 2006-04-26 |
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